Rotating drum coating apparatus



June 24, 1969 F. MARTIN 3,451,375

ROTATING DRUM COATING APPARATUS Original Filed Sept. 15, 1964 Sheet of Inventor FRITHJOF MARTIN June 24, 1969 M T I 3,451,375

ROTATING DRUM COATING APPARATUS Original Filed Sept. 15, 7,964 Sheet 4 of 2 FRITHJOF MARTIN a; 2 1753%, N0 :1 @MM 'H-H'orn egs United States Patent 3,451,375 ROTATING DRUM COATING APPARATUS Frithjof Martin, Bern, Switzerland, assignor to Dr. A. Wander S.A., Bern. Switzerland, a Swiss corporation Original application Sept. 15, 1964, Ser. No. 396,498, now Patent No. 3,390,648, dated July 2, 1968. Divided and this application Jan. 3, 1967, Ser. No. 606,814 Claims priority, application Switzerland, Sept. 19, 1963, 11,597/63 Int. Cl. B05c 7/02 US. Cl. 118-19 6 Claims ABSTRACT OF THE DISCLOSURE A tablet coating apparatus having a rotating drum with the interior of the drum having a profiled friction surface or lining to which the tablets tend to adhere more readily than to each other when the drum is rotated.

This application is a divisional application of US. application Ser. No. 396,498, filed Sept. 15, 1964 now U.S. Patent No. 3,390,648, issued July 2, 1968.

The invention concerns a procedure for coating particles, such as tablets of, for instance, biconvex shape, and in particular those produced by the pharmaceutical industry.

Technical progress reached in this field is described in a paper by K. Munzel entitled, Neuenungen auf dem Gebiet der pharmazeutischen Dragierung (Innovations in the Field of Pharmaceutical Coated Tablet Manufacturing). This appeared in the journal, Pharmaceutica Acta Helvetiae, Nos. 2 and 3, of 1963. The disadvantages of the traditional method of sugar-coating cores in a pan have prompted suggestions for improvement, both as regards the coating substance used and the process and equipment, respectively. These disadvantages relate to the time required-anywhere from a few hours to several daysfor the coating process and the need of a skilled staff to supervise and direct it; the insufficient theoretical command of the process, making quality variations and ruined batches inevitable; and the considerable increase in the weight of the tablets with need of correspondingly larger packages and transportation costs, among other things, besides the so-called rapid coating procedures and the sugarless-coating procedures with substances soluble in water, the lacquering method has recently acquired practical importance. This involves applying to the core a solution preferably film-forming, dissolved in an organic solvent.

In the well known lacquering technique, the lacquer solution is poured or preferably sprayed on to the mass which is revolved in the conventional pan, whereby volatilization of the solvent can be aided by introducing heatfor instance, by radiation or the blowing on of hot airand sucking 01f the solvent vapors.

The unavoidable abrasion when a pan is used, batches of from 20 to 50 kg. and more being rolled around for hours, is far more disadvantageous in the lacquering procedure, in which the coating is very thin. In the sugarcoating method this abrasion is to some extent desirable (in the initial stage because of the rounding-off of the 3,451,375 Patented June 24, 1969 process, assisted by heat, there is the additional factor that the film is formed essentially on the free surface of the mass of tablets. The larger this mass, the more unfavorable (in a potentiated ratio) for the individual tablets the ratio between the travel time in which they are exposed to the coating processes, and the time during which the negative influences (abrasion of core substance and its incorporation into the covering layer, impairing of the coating already formed) prevail; in addition, the bigger will be the deviations from the statistical mean of the travel time in which the individual tablets are on the free surface. This again results in greater variation in the attained thickness of the film.

To compensate for these disturbing factors and to guarantee sufficient probability that the coating will never drop below a certain minimum thickness, when using the lacquering process in a pan, one must still reckon with a comparatively lengthy processing time (with correspondingly high abrasion) and a sizable average thickness of the coating. In the case of largish pans some 15' sprayings will be needed, requiring about four hours working time. The brasion resistance must then be even higher than with the sugar-coating process. On the other hand, leaving out economic considerations, there is a lower limit for the mass of tablets (batch) being made in one operation through the fact that with given dimensions of the pan the required revolution of the cores can only be guaranteed with a certain minimum loading. Should this critical limit not be reached, the mass as a whole begins to slide, causing it merely to oscillate.

If one uses for the lacquering process drums rotating around their horizontal axis, instead of pans, as already proposed for the conventional sugar-coating (see French Patent No. 1,288,469), the problems are basically the same as when using a pan.

By changing over to the fluidized bed process, as described for instance in the British Patent No. 899,900, it was possible to reduce considerably the processing time (to about half an hour to one hour). However, the abrasion of the cores against each other is no less than in the pan. In addition, a good deal more equipment is needed than for the conventional coating process, so that the fluidized bed method has not so far gained any extensive practical importance.

The invention presented here is based on the perception that both in lacquering in the pan or in the drum, as well as in the fluidized bed equipment, far too large batches of tablets are, or have to be handled. In my own experiments I observed the movements of marked tablets in batches andin part specially equippedpans of various sizes, and in particular I determined the ratio of the travel time of the tablets between appearing on the surface and disappearing into the mass, and vice versa, as well as the incidence of this ratio. In addition, I examined under varying working conditions the abrasion of core substance and the damage done to partially formed films. This showed that the inherent advantages of lacqueringsuch as shortening of the operation period, reduction of the thickness of the coating and better control of the process itselfcould only be partially utilized when employing the usual equipment, for the reasons already mentioned, and that these and other factors can be greatly improved by adopting the process of my invention.

In my invention the lacquering is done in a drum rotating round its horizontal axis. By contrast with conventional methods, this drum contains such a small batch of tablets that with the usual smooth nature of the inner surface of the drum there would be no revolving motion. With such a smooth inner surface it is generally necessary to fill the drum to a minimum of about 10% of its volume to assure a revolving motion, whereas with the procedure 3 invented by me the volume of the drum filling is considerably inferior to Notwithstanding this, so that the batch of tablets will revolve, in my invention the inner surface of the drum must be such that the tablets slide much less well against it than among themselves. In my invention, the layer of the revolved tablet batchhereafter called the revolving layermust in addition have a maximum height which lies between three times the smallest and ten times the largest diameter of the tablets.

These conditions are found to be advantageous not only for the lacquering of tablets but also for other procedures intended to provide particles with a covering coating, in which there are similar governing criteria as in the lacquering of tablets. The invention thus is concerned with a new procedure for coating particles, such as tablets of, for instance, biconvex shape, and in particular those produced by the pharmaceutical industry, especially by spraying on a lacquer solution, which comprises revolving the particles while being coated in the interior of a drum rotating round its horizontal axis, the inner surface of the drum being of such a nature that the particles slide considerably better among themselves than against it, said particles forming a revolving layer occupying considerably less than 10% of the internal volume of the drum, the maximum height of the revolving layer being between three times the smallest and ten times the largest diameter of the particles.

The particles constituting the revolving layer resulting from the arrangement described must necessaril follow a movement which i characterized by two turning points with two accelerating stretches in between. From the lower turning point, roughly corresponding to the lowest point of the drum, the particles are conveyed in forward motion according to the rotating speed of the drums surface in a circular path to the upper turning point. From here, under the influence of gravity, they drop back to the lower point, sliding more or less straight over the particles conveyed upwards. Since the acceleration in the field of gravity is independent of weight, the dynamics of the revolving layer is largely independent of the size and weight of the particles.

The adhesion of the particles to the inner surface of the drum, which is necessary in the new procedure, can be achieved, for instance, by cladding the surface with a profiled rubber lining or something similar. The essential point is that the particles resting on the surface and those immediately next to them are drawn along by the ascending drum wall, so that the desired revolving motion can actually develop and that the load in its entirety does not slide down along the ascending drum surface, as would be the case with the thin layer of my invention, if no special measures were taken to increase adhesion.

While the particles slide back from the upper to the lower turning point, the lacquer solution is sprayed on, and this can be accompanied by direct heating by means of radiation or adduction of hot air. Because all the particles must of necessity pass regularly under the spray, the coating is extremely regular, with minimum deviations from the standard value and without being affected by abrasion of the cores or damage to the coating, because the revolving layer is not very high. As the thickness of the coating depends very closely on both the apparatus factors and the duration of the operation, films of a thickness of, if desired, about l() cm. can be formed with a high degree of accuracy and without any danger of bare spots. The coating operation is completed within a few minutes because of this and also as a result of the extremely favorable ratio, for every single particle, between spraying time and idle time, i.e., the time during which no spraying is done, This is why, with a comparable amount of equipment, and despite relatively small batches, production is much greater with the device developed by me than with the traditional pans, drums or fluidized equipments.

Simultaneous coating of larger quantities of particles, with the other dimensions remaining identical, requires a correspondingly longer drum. In this case, the inner surface of the drum is suitably subdivided by means of circular ribs or lamellae into channels, the width of which is from three to ten times the maximum diameter of the particles. It is even more advantageous if these ribs are interconnected to form a helical track, so that the particles being coated are moved axially on this track through the rotating drum.

My process can be carried out either by feeding one batch at a time, or continuously. In the former case, one or several circular tracks on the inner surface of the drum will sufiice. One way of taking the particles out is by inserting after the coating is finished specially fitting collectors in the tracks ahead of the lower turning point and allowing these to be taken up to the upper point. In this way, the particles are caught by the container instead of returning to the lower turning point. New particles can be loaded by inserting similar containers holding the desired batch, which can be dropped into the rotating track by inserting containers holding the desired batch with said containers being open at the back side thereof with respect to the direction of rotation of the drum, and by allowing the containers to be moved within the drum from the lowest point therein to the upper turning point. Both operations can be carried out without stopping the drum, in one single operation which can be made automatic. Other methods of loading and unloading will be evident to the specialist-for instance through openings in the drum surface can be closed by sliders, b conveyer belts, silo-like storage containers, and similar devices.

If the track of the revolving layer on the inner wall of the drum is of the helical type, loading need only be done at the beginning of the helical track, and this can be done either batchwise (one per revolution of the drum), or continuously In continuous loading, the first helical revolution collects the batch, which is conveyed axially through the drum; in order to prevent disparities, spraying should in thi case be done only from the second turn of the helix onwards. At the end of the helical track batches of coated particles need only be collected. With this continuous method, the operating time is determined by the characteristics of the apparatus. This time can, however, be varied by loading the particles in a later turn instead of in the first one.

In the prcess described here the rotary speed of the drum and the intensity of the spraying are variable within certain limits. These values have, however, certain optima which can be determined empirically and depend on the particles and coating solutions used, and there should be no great deviations from these optima. There is also an optimum for the quantity of particles which can be treated in one turn of the track on the interior surface of the drum. Obviously, revolving layers which are too large and particularly too high would partially cancel out the advantages sought by my process.

Therefore, the maximum height of the revolving layer must be inferior to ten times the largest diameter of the particles; however, it way not be inferior to three times the smallest diameter of the particles because otherwise an actual revolution of the layer would no longer be assured. In the case of biconvex pharmaceutical tablets of usual size, batches of from to 1,000 grams are preferred in the lacquering technique in accordance with the invention.

For spraying, the well known mixing jets can advantageously be used, it being possible to vary the air pressure and the supply of solution. The airstream conveying the solution possesses a remarkable jet pressure which, though as with nearly all spraying systems (except for electrostatic ones) causes substance to be lost, oifers considerable advantages. The air streaming in with particles of solution at the same time removes any dust which may be adhering to the tablets, so that no foreign substances can penetrate the film. In addition, there is a physical-mechanical film formation, which also produces adherent films on apparently smooth nonporous tablet surfaces. The paper mentioned earlier and certain references quoted in it contain many suggestions as to the composition of the spray solutions. In addition to lacquer solutions in the proper sense, for the application of which my process is particularly suited, consideration can also be given to aqueous solutions as well as aqueous and nonaqueous suspensions of substances which are preferably film forming.

The invention is explained by Way of example by means of the accompanying drawing, wherein:

FIG. 1 is a schematic diagram, partly sectional, of the equipment for continuous working;

FIG. 1A is a fragmentary schematic diagram, partially sectional, of a modified form of the equipment for coating tablets or other particles;

FIG. 2 is a perspective view, showing a section of the interior of the drum in which the tablets or other particles are coated; and

FIG. 3 is a schematic presentation of the revolving layer in the cross-sectioned drum.

A horizontally positioned drum 1 rests at both ends on pairs of rollers 2 which turn in bearings 3 mounted on a base 4. One or more of these rollers can be set turning by means of an electromotor 5 to rotate the drum I slowly and regularly. On the inner surface of the drum and at right angles to its axis is a continuous helicoidal riFTn lamella 6 broadened at its base to form a helical groove 7 which in cross-section has a concave bottom lined with profiled rubber 8.

In the groove 7 are the tablet batches 9, which when the drum 1 rotates take the shape and dynamic of a revolving layer with a lower turning point 10, an upper turning point 11, a forward acceleration stretch 12 and a backward acceleration stretch 13.

Arranged along the interior of the drum 1 are several sprayers 14 aimed at the backward acceleration stretch 13 of the revolving layers formed by the tablet batches 9. These sprayers are connected to a common compressedair duct 15 and to individual solution supply ducts 16 fed from a container 17 (or fed individually or in groups from several such containers). This container is put under pressure by means of a compressed air duct 18 which also feeds the duct 15, and during filling the air can be let out by opening a valve 19. In the ducts 15, 16 and 18 there are regulating valves 20 as well as pressure gauges, flow meters, etc. A duct 21 extending horizontally through the interior of the drum, and also equipped with a regulating valve 20, has side nozzles (not shown) pointing downwards, through which hot air is blown. Above this extends through the interior of the drum a suction duct 22 connected to a suction pump 23 and having a large number of openings to remove solvent vapors from the drum. Numeral 24 represents a device for feeding tablets to the one end of the helical groove 7, and numeral 25 represents a device for removing the coated tablets. For example, the tablet feeding device 24 can be a simple mechanical means for discharging at regular intervals into the grooves 7 a weighed amount of the tablets or, if preferred, a continuous stream of tablets can be fed to the groove 7 by means of a vibrating feed drum in the manner described hereto in column 4, lines 14-15.

The modified form of the coating equipment illustrated in FIG. 1A comprises a horizontally positioned drum 1a supported at opposite ends on pairs of rollers 2a which turn in bearings 3a mounted on a base 4a. An electromotor 5a turns one or more of the rollers 4a. On the inner surface of the drum 1a and at right angles to the axis thereof are a plurality of spaced circular ribs or lamellae 6a defining therebetween circular grooves 7a which in cross-section have a concave bottom and which preferably are lined with profiled rubber to provide an interior friction surface.

The process for coating tablets or other particles is carried out by the above described continuously operating equipment as follows:

A small quantity of the cores to be coated is fed continuously or at intervals into the slowly rotating drum 1 by the device 24. These quantities move from one end of the drum to the other through the drums rotation and the force of gravity, and are thereby coated in the way already described. Each quantity of tablets 9 contained in a lower section of the helical groove 7 goes through a revolving motion, the tablets lying on the surface of the revolving layer being especially exposed to the spray from the nozzles 14. The particles sprayed on, dry almost immediately with the aid of the hot air blown on to them.

EXAMPLE Rotating drum 1:

Length 140 cm. Diameter cm.

Revolution speed of the drum 5 rpm. Width of the helical groove 7 3.5 cm. Height of the helical groove 7 6 cm. Number of turns of the helical groove 7 35.

Hot air directed on the upper turning point 11 of the tablets, temperature About 4060 C. Quantity of tablets fed per drum revolution About 300 g. Weight of a single biconvex tablet 0.5 g. Maximum diameter of a tablet 0.6 cm. Maximum height of the revolving layer 4 to 5 cm.

This gives for traveling through the 35 turns of the helical groove 7 an operating time of seven minutes and a capacity of 1.5 kg. of tablets per minute or kg. of tablets per hour.

The spray jets may be in the form of mixing jets or compressed solution jets. If desired, using the continuous process, coatings of various kinds can be applied succes sively through different sprayers in the same operation. In addition to or instead of the hot air drying, radiant heat drying can also be used. Hot air can be blown on to the rotating layer of tablets, either against or in the safe direction. The tablets can be fed in measured quantities by simple mechanical means, by a controlled vibrator or similar means. The process can also be carried out in a vacuum in order to speed up the drying of the solution.

The procedure described here permits the continuous lacquering of tablets by means of a relatively simple and extremely efficient device, without requiring qualitifed staff, or even completely automatically. As the operating time is brought down to only a few minutes, and no considerable mechanical forces are employed, there is practically no abrasion, even in the case of less hard cores, and the coating being formed is not adversely affected either mechanically or through abrasion. The thickness of the coating can be predetermined with great accuracy. Even with extremely thin coatings which. allow dividing grooves and recessed identifying markings on the surface of the tablets to remain, there are no bare spots.

The process is chiefly suitable for covering particles produced by the pharmaceutical industry, such as pills, tablets of various shapes and sizes, capsules and so on, with a coating which gives the core beneath it protection, improved taste, more attractive appearance, resistance to the gastric juices and other advantages. It can, however, also be used for other purposes, where particles in large quantities have to be provided reliably and accurately with a thin covering film.

I claim:

1. In an apparatus for spray coating particles, such as tablets of biconvex shape produced by the pharmaceutical industry, in a rotating coating drum the improvement which comprises; a coating drum having a generally cylindrical interior surface which is rotatable about the longitudinal axis of said drum on a generally horizontal axis, said coating drum having associated therewith spray means for introducing into the interior thereof liquid material suitable for coating said particles, and said coating drum having the said interior surface thereof subdivided into circular grooves each having a generally concave bottom surface, and said concave bottom surface being provided with a profiled friction lining.

2. An apparatus as in claim 1, wherein said profiled friction lining is a profiled friction rubber lining.

3. An apparatus as in claim 1, wherein said spray means is adapted to introduce into the interior of said drum liquid lacquer material suitable for coating the said tablets.

4. In an apparatus for spray coating particles, such as tablets of biconvex shape produced by the pharmaceutical industry, in a rotating coating drum the improvement which comprises; a coating drum having a generally cylindrical interior surface which is rotatable about the longitudinal axis of said drum on a generally horizontal axis, said coating drum having associated therewith spray means for introducing into the interior thereof liquid material suitable for coating said particles, and said coating drum having the said interior surface thereof subdivided into a continuous helical groove having a generally concave bottom surface, and said concave bottom surface being provided with a profiled friction lining.

5. An apparatus as in claim 4, wherein said profiled friction lining is a profiled friction rubber lining.

6. An apparatus as in claim 4, wherein said spray'means is adapted to introduce into the interior of said drum liquid lacquer material suitable for coating the said tablets.

References (Iited UNITED STATES PATENTS 901,455 10/1908 Lauhoif 118-303 X 3,167,035 1/1965 Benson 118--19 X 1,910,536 5/1933 Guggenheim 1181-9 X 2,994,165 8/1961 Brevik 259- 81 X 3,095,326 6/1963 Green et a1 11819 X 3,138,368 6/1964 Park et al. 259-81 3,220,875 11/1965 Queneau 117109 X 3,285,223 11/1966 Sahlin 118-418 X 2,298,016 10/1942 Lincoln 2593 X 2,560,820 7/1951 Recker 118 19 X 3,172,644 3/1965 Smith 259-"8l ROBERT W. MITCHELL, Primary Examiner.

I. P. MCINTOSH, Assistant Examiner.

US. Cl. X.R. 1l824 

